CN2414064Y - Gas dissolving pipe - Google Patents
Gas dissolving pipe Download PDFInfo
- Publication number
- CN2414064Y CN2414064Y CN 99229268 CN99229268U CN2414064Y CN 2414064 Y CN2414064 Y CN 2414064Y CN 99229268 CN99229268 CN 99229268 CN 99229268 U CN99229268 U CN 99229268U CN 2414064 Y CN2414064 Y CN 2414064Y
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- Prior art keywords
- pipe
- inlet pipe
- distribution plate
- air distribution
- air
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- Expired - Lifetime
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Abstract
The utility model relates to an environment protecting technology, particularly an air dissolving pipe dissolving air in water, comprising a pipe body, a clear water inlet pipe and a dissolved-air water outlet pipe both arranged on the pipe body in which an air distributing plate is arranged. Both ends of the pipe body are connected with end caps. A flow deflector in the air distributing plate is provided with an air spraying pipe of which one side is uniformly distributed with micropores along the axial direction, and the other side is connected with an air inlet pipe, wherein, the micropores and the air inlet pipe are respectively arranged on two planes of the flow deflector. The other end of the air inlet pipe is extended out of the pipe body.
Description
The utility model relates to green technology, and is specifically a kind of with the device of air dissolves in water.
When disposing of sewage, need utilize air soluble method that water is carried out molten gas with the air supporting method.The main points of air soluble method are to tell a part through the clear water after purifying in the air flotation pool, to pump in the dissolving with reflux pump, and make it to keep certain pressure, to feed the high slightly pressurized air of pressure simultaneously.Water needs to be detained for some time in dissolving, and air can be dissolved in the water gradually by diffusion.The pressure water of molten water air is called dissolved air water.Dissolved air water suddenly is decompressed to normal pressure after discharging, air soluble in water becomes the supersaturation attitude suddenly, so in water, evaporate rapidly, form small bubble, this water that is full of microbubble is imported air flotation pool, mix with the sewage after the dosing flocculation, microbubble can combine with flocs unit, and with its picking-up, floating to water surface formation scum silica frost, use the Scraping device descum, sewage just is purified.
The dissolved-air rate of dissolving is high more, and the microbubble concentration after not only discharging is high more, and the degree of supersaturation of molten gas is also big more when discharging, the speed that molten gas evaporates in water is faster, the microbubble that forms is directly through littler, and the two all can improve air flotation effect, and purification rate is improved.
But the present dissolving that uses, its molten gas principle is based on the diffusion of gas molecule, thereby dissolving is quite big, and molten gas efficient but has not high.
The purpose of this utility model is that design is a kind of simple in structure, the high Gas dissolving pipe of molten gas efficient.
Its main technical schemes comprises a body and is installed in clear water inlet pipe and dissolved air water outlet pipe on this body, air distribution plate is arranged in body, the two ends of body connect end cap, a gas ejector pipe is arranged on the flow deflector in air distribution plate, at the uniform vertically micropore of a side of this gas ejector pipe, opposite side connects inlet pipe, and wherein micropore and inlet pipe lay respectively on two planes of flow deflector, and the other end protruded tube of inlet pipe is external; One segment distance n is arranged between the medullary ray of clear water water inlet pipe and the medullary ray of body, outward-dipping angle α is arranged between the medullary ray of clear water inlet pipe and the transverse section of body, air distribution plate is positioned at the opposite of clear water inlet pipe, and and the inwall of body between angle β is arranged, the two ends of air distribution plate utilize fixed link to be installed in the inwall of body respectively: inlet pipe is positioned at the middle part of gas ejector pipe, the outer end of inlet pipe is positioned at the saddle flange on the outer wall that is installed in body, and between inlet pipe and saddle type method are put, sealing-ring is set, chew at the end of saddle flange connection Intake Cover and gas, between Intake Cover and saddle type method gas, gasket is set; In the clear water inlet pipe, the jet pipe of tubular is connected with body, and the upper end of jet pipe connects special-shaped hydraucone, and at the bell-mouthed end of abnormity joint flange, the outside inwall of jet pipe and the inwall of body are tangent; The transverse shape of flow deflector can be plate shaped or arc in the air distribution plate, if during arc, the connection transverse slat at its two ends also is an arc, between the port of clear water inlet pipe and body, utilize to take over and be connected ball valve, manage intravital air distribution plate and can install 1, two or more, stagger mutually in the installation site of every air distribution plate.
The utility model has the advantages that molten gas efficient height, the recirculation water that comes when the reflux pump pump is from jet pipe when α and certain speed are spurted in the body at a certain angle, in the L section, because the shock action of jet pipe current is managed intravital water and begun to rotatablely move as volution on whole cross section.When being used as water that spirrillum rotatablely moves and being advanced into the air distribution plate position, its fluidised form is as shown in figure 10: the outer current between tube wall and the air distribution plate keep corkscrew motion substantially, and at C point place, the water that is rotating is because of being subjected to stopping of flow deflector, be forced to change direction, be close to the air distribution plate motion.Tangential speed is bigger at A point place.At this moment, spray in the micropore of pressurized air with very high speed gas ejector pipe on air distribution plate, the place enters in the water body at the A point.If micro-pore diameter, pitch-row and compressed air pressure, flow are selected proper, the micro-air stream that enters in the water will be dissolved rapidly fully, the water that dissolves in behind the air is withdrawn the A point rapidly, the water that its position is not dissolved in air immediately replaces, this has just realized water--sharp acute change that the gas contact is mutual, thus accelerated molten gas process greatly.
Because whenever to revolve the water layer that dissolves in air of turning around very thin for water body in the pipe, so air distribution plate must have certain length, and setting angle β arranged, so, along with the spirrillum of water body is rotated, air is able to dissolve in continuously layer by layer.
The setting angle α of jet pipe has determined the helix angle of water body spiral motion in the gas, generally must get α≤β.So, because the reflex action of air distribution plate, the water body of air distribution plate inboard will not advance along the body axial direction due, sometimes retreat slightly on the contrary, that pushes ahead only is the ring-type water layer between inside pipe wall and the air distribution plate, this water layer spirrillum is advanced into body solution water out place, discharges body, enters reliever.Be not difficult to find out that the water that A point place must have been dissolved in air is directed at the outer ring, the flow deflector of air distribution plate upside has played this effect.Owing to produce negative pressure near the existence of the flow deflector of air distribution plate upside, B point, add the tangential speed height of A point place water, dissolved in the water behind the air and dashed to the outer ring.Between the ratio of choose reasonable α and β, air distribution plate width H, air distribution plate and the inboard wall of tube body apart from △, the water that can guarantee to dissolve in behind the air arrives inboard wall of tube body at D point place.
At D point place, owing to sneaking into of A point place current, External Cordon Line speed will increase, and the kinetic energy of its increase is passed to heart portion water body gradually in rotary course, and the water body rotation of heart portion is quickened, and External Cordon Line speed is to recovering normal near the E point again.It is proper only to need each parameter to select, and can make the current tangential speed at A point place on each cross section constant substantially, guarantees that promptly the resistance in each micropore aperture of air distribution plate gas ejector pipe is constant substantially, that is guarantee that the jet amount of each micropore is constant substantially that molten gas effect reaches optimum value.
Pipe diameter φ, length L, jet pipe flow velocity V, jet pipe installation angle α, air distribution plate is to the distance 1 of jet pipe, air distribution plate length, air distribution plate and inboard wall of tube body be apart from △, air distribution plate width H, air distribution plate setting angle β, micropore size and pitch-row, the radius-of-curvature of arc air distribution plate are the important parameters of this dissolved-gas pipe.
Fig. 1 is a structure iron of the present utility model.
Fig. 2 is the vertical view of Fig. 1.
Fig. 3 is the F-F view of Fig. 1.
Fig. 4 is the air distribution plate structure iron.
Fig. 5 is the K-K view of Fig. 4.
Fig. 6 is the G-G view of Fig. 4.
Fig. 7 is the G-G view when the air distribution plate among Fig. 4 is arc.
Fig. 8 is the structure iron after the two joint Gas dissolving pipe assemblings.
Fig. 9 is the structure of placing two air distribution plates in every joint Gas dissolving pipe.
Figure 10 is fluid kinestate sectional drawing in body.
As shown in the figure: the two ends at body 12 connect end cap 1, connect the clear water inlet pipe in the left side of body 12, and the right side connects dissolved air water outlet pipe 13.Jet pipe 11 in the clear water inlet pipe is tubular, jet pipe is connected with body 12, the inwall in the jet pipe outside and the inwall of body are tangent, connect special-shaped hydraucone 10 in the jet pipe upper end, and at its end joint flange 9, between the end cap 1 in special-shaped hydraucone 10 and left side, utilize and take over 5, elbow 6, casing coupling 7 be connected ball valve 8, on the end cap on body right side, utilize pipe connecting 15 to connect stopping valve 16, at the upper end of dissolved air water outlet pipe 13 joint flange 14, between each end cap at body 12 two ends, gasket 2 is installed.
Opposite side with respect to the clear water inlet pipe in body 12 utilizes air distribution plate fixed link 23,17 that air distribution plate 18 is installed, air distribution plate is made of the connection transverse slat 28 at flow deflector 29 and two ends thereof, a gas ejector pipe 30 is longitudinally arranged at the middle part of flow deflector, at the densely covered vertically micropore 32 of a side of gas ejector pipe, the middle part of opposite side connects inlet pipe 27.The transverse shape of air distribution plate can be plane, also can be arc, as 29 ' among Fig. 7.During installation, the side direction body center that micropore is arranged, inlet pipe is stretched out body, connect a saddle flange 22 at tube wall, the outer end of inlet pipe is positioned at this saddle flange, connects Intake Cover 20 in the upper end of saddle flange, and gasket 19 is set between Intake Cover and saddle flange, 0 shape sealing-ring 21 is arranged between inlet pipe 27 and saddle flange, on Intake Cover, have gas to chew 26.
As required, two Gas dissolving pipes can be in series, as shown in Figure 8, at this moment, on the Gas dissolving pipe clear water inlet pipe be arranged, the dissolved air water outlet pipe is arranged on another root.Also can as shown in Figure 9 two relative air distribution plates be installed in every Gas dissolving pipe.
Claims (8)
1, a kind of Gas dissolving pipe, comprise body (12) and be installed in clear water inlet pipe and dissolved air water outlet pipe (13) on the body, air distribution plate (18) is arranged in body, body (12) two ends connect end cap (1), it is characterized in that on the flow deflector (29) in the air distribution plate (18) gas ejector pipe (30) being arranged, at the uniform vertically micropore of a side of this gas ejector pipe (30) (32), opposite side connects inlet pipe (27), wherein, micropore (32) lays respectively on two planes of flow deflector (29) with inlet pipe (27), and the other end of inlet pipe (27) stretches out outside the body (12).
2, Gas dissolving pipe according to claim 1, it is characterized in that between the medullary ray of the medullary ray of clear water inlet pipe and body (12) a segment distance n being arranged, outward-dipping angle α is arranged between the transverse section of the medullary ray of clear water inlet pipe and body (12), air distribution plate (18) is positioned at the opposite of clear water inlet pipe, and and the inwall of body (12) between angle β is arranged, the two ends of air distribution plate (18) utilize fixed link to be installed on the inwall of body (12) respectively.
3, Gas dissolving pipe according to claim 1, it is characterized in that inlet pipe (27) is positioned at the middle part of gas ejector pipe (30), the outer end of inlet pipe is positioned at the saddle flange (22) on the outer wall that is installed in body (12), and between inlet pipe (27) and saddle flange (22), sealing-ring (21) is set, chew (26) at the end of saddle flange (22) connection Intake Cover (20) and gas, between Intake Cover (20) and saddle flange (22), gasket (19) is set.
4, Gas dissolving pipe according to claim 1, it is characterized in that in the clear water inlet pipe, the jet pipe of tubular (11) is connected with body (12), the upper end of jet pipe (11) connects special-shaped hydraucone (10), at the end joint flange (9) of special-shaped hydraucone (10), the inwall of the outside inwall of jet pipe (11) and body (12) is tangent.
5, Gas dissolving pipe according to claim 1 is characterized in that the transverse shape of the flow deflector (29) in the air distribution plate (18) is plate shaped.
6, Gas dissolving pipe according to claim 1 is characterized in that the transverse shape of the flow deflector (29) in the air distribution plate (18) is an arc, and the connection transverse slat (28) at its two ends is also curved.
7, Gas dissolving pipe according to claim 1 is characterized in that utilizing between the end cap (1) of clear water inlet pipe and body (12) and takes over (5) and be connected ball valve (8).
8, Gas dissolving pipe according to claim 1 is characterized in that the air distribution plate (18) in the body (12) can be installed 1, two or more, staggers mutually in the installation site of every air distribution plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99229268 CN2414064Y (en) | 1999-08-27 | 1999-08-27 | Gas dissolving pipe |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99229268 CN2414064Y (en) | 1999-08-27 | 1999-08-27 | Gas dissolving pipe |
Publications (1)
Publication Number | Publication Date |
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CN2414064Y true CN2414064Y (en) | 2001-01-10 |
Family
ID=34018530
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 99229268 Expired - Lifetime CN2414064Y (en) | 1999-08-27 | 1999-08-27 | Gas dissolving pipe |
Country Status (1)
Country | Link |
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CN (1) | CN2414064Y (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104502339A (en) * | 2014-09-15 | 2015-04-08 | 中国纺织信息中心 | Method for detecting content of non-destructive formaldehyde of textile |
CN104568792A (en) * | 2014-09-15 | 2015-04-29 | 中国纺织信息中心 | Equipment for detecting content of non-destructive formaldehyde in textile |
CN106823875A (en) * | 2017-04-11 | 2017-06-13 | 无锡沪东麦斯特环境科技股份有限公司 | A kind of highly effective air dissolver |
CN107008168A (en) * | 2017-05-19 | 2017-08-04 | 北京东方同华科技股份有限公司 | A kind of two grades of air dissolving systems of single cycle and its molten gas method |
CN109607657A (en) * | 2018-12-26 | 2019-04-12 | 广西粤桂广业控股股份有限公司 | A kind of centrifugation flotation tank |
-
1999
- 1999-08-27 CN CN 99229268 patent/CN2414064Y/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104502339A (en) * | 2014-09-15 | 2015-04-08 | 中国纺织信息中心 | Method for detecting content of non-destructive formaldehyde of textile |
CN104568792A (en) * | 2014-09-15 | 2015-04-29 | 中国纺织信息中心 | Equipment for detecting content of non-destructive formaldehyde in textile |
CN106823875A (en) * | 2017-04-11 | 2017-06-13 | 无锡沪东麦斯特环境科技股份有限公司 | A kind of highly effective air dissolver |
CN107008168A (en) * | 2017-05-19 | 2017-08-04 | 北京东方同华科技股份有限公司 | A kind of two grades of air dissolving systems of single cycle and its molten gas method |
CN107008168B (en) * | 2017-05-19 | 2023-10-31 | 北京东方同华科技股份有限公司 | Single-cycle two-stage gas dissolving system and gas dissolving method thereof |
CN109607657A (en) * | 2018-12-26 | 2019-04-12 | 广西粤桂广业控股股份有限公司 | A kind of centrifugation flotation tank |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee |
Free format text: FORMER NAME OR ADDRESS: XISHAN HUDONG METALLURGICAL ENGINEERING MACHINERY MFG. CO., LTD. |
|
CP03 | Change of name, title or address |
Address after: Qian Qiao, Hua Zhen Town, Binhu District, Wuxi, Jiangsu Patentee after: Wuxi Hudong Metallurgical Engineering Machinery Manufacturing Co., Ltd. Address before: Qian Qiao Qiao Hua Town Xishan city Jiangsu Province Patentee before: Ludong Metallurgical Engineering Machinery Manufacturing Co., Ltd., Xishan City |
|
C17 | Cessation of patent right | ||
CX01 | Expiry of patent term |